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Process Equipment and Plant Design

Process Equipment and Plant Design
The safe height (h) to diameter (d) ratio (i.e., h/d) for liquid/petro fuel storage tank of capacity more than 45 kilolitres is less than

3
2
1
3.5

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Process Equipment and Plant Design
Large process vessels operating under extreme temperature and pressure conditions are normally clad/ lined with materials like stainless steel, aluminium, nickel & its alloys, copper & its alloys and titanium. The cladding thickness is generally about __________ percent of the total thickness.

40 to 50
10 to 20
1 to 5
30 to 40

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Process Equipment and Plant Design
An adequate clearance between the tray and the shell wall of a distillation column is provided to

None of these
Avoid back-trapping
Allow for thermal expansion and facilitate installation
Drain the liquid from the tray when the unit is not in operation

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Process Equipment and Plant Design
In the design of a bag filter, the gas temperature is an important consideration, as it affects the

Gas density
Fibre selection
All of these
Gas viscosity

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Process Equipment and Plant Design
Which of the following is not a graphical method (but is an analytical method) for the calculation of theoretical number of stages in case of continuous binary distillation?

None of these
McCabe-Thiele's method
Ponchon-Savarit method
Sorel-Lewis method

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Process Equipment and Plant Design
Larger depth of liquid on the trays of a distillation column

Both A & B
Leads to high tray efficiency
Results in higher pressure drop per tray
Neither A nor B

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